CN1740129A - Prepn process of hydroquinone and phenol - Google Patents
Prepn process of hydroquinone and phenol Download PDFInfo
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- CN1740129A CN1740129A CNA2005100320710A CN200510032071A CN1740129A CN 1740129 A CN1740129 A CN 1740129A CN A2005100320710 A CNA2005100320710 A CN A2005100320710A CN 200510032071 A CN200510032071 A CN 200510032071A CN 1740129 A CN1740129 A CN 1740129A
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- catalyst
- oxygenant
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- benzene
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
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- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The preparation process of hydroquinone and naphthol has phenol, aniline, naphthaline or their substitutent as material; and hydrogen peroxide, sodium hypochlorite or air as oxidant; and includes reaction of the material and the oxidant in the molar ratio of 1 to 0.5-5 inside various solvent of pH value 1-13 at 25-200 deg.c and 1-20 atm for 1-5 hr in the presence of catalyst. The catalyst is monometal porphyrin, or module-oxy bimetal porphyrin with or without inorganic or organic high molecular matter in the concentration of 2-500 ppm, and the catalyst may have co-catalyst in the molar number of 1-20 time that of the main catalyst. The present invention has mild reaction condition, less catalyst consumption, high catalytic efficiency, high reaction selectivity, no corrosion to apparatus, high conversion rate and high yield.
Description
Technical field
The present invention relates to the catalyzed oxidation preparation method of a kind of dihydroxy-benzene and naphthols.
Background technology
Dihydroxy-benzene and naphthol compound are important chemical material and intermediate.What use was maximum at present is with hydrogen peroxide oxidation phenol coproduction pyrocatechol and Resorcinol under catalyst action.EP 432006 and EP408418 disclose with HClO
4Be catalyzer, H
3PO
4Being promotor, is the method for raw material production dihydroxy-benzene with the hydrogen peroxide of phenol and 70%, and US 4078006 discloses with H
2SO
4With mibk be catalyzer, with phenol and hydrogen peroxide is the method for raw material synthesizing benzene diphenol, it is catalyzer that EP 480800 discloses with molysite and cobalt salt mixture, hydrogen peroxide with phenol and 60% is the method for raw material production dihydroxy-benzene, it is catalyzer that US 4410501 discloses with the HTS with MFI structure, hydrogen peroxide with phenol and 30% is the method for raw material production dihydroxy-benzene, it is catalyzer that CN 1328873 discloses by complex metal oxides, is the method for raw material production dihydroxy-benzene with phenol and hydrogen peroxide.Have plenty of catalyzer in the aforesaid method equipment is had corrosive nature, have plenty of transformation efficiency and the rate of recovery is low.
Summary of the invention
The object of the present invention is to provide does not a kind ofly have corrosive nature to equipment, can improve the method for the transformation efficiency and the rate of recovery.
Technical scheme of the present invention is: with phenol, aniline, naphthalene or their substituent are made raw material, at pH 1～13 water, acetone, ethanol, acetate, ethyl acetate, benzene, in the toluene equal solvent, select for use by the μ-oxygen bimetallic porphyrin of the monometallic porphyrin of general formula (I) or general formula (II) or above-mentioned metalloporphyrin and inorganic or immobilized thing that organic polymer constitutes separately as catalyzer, catalyst concn is 2-500PPM, use hydrogen peroxide, clorox or air are as oxygenant, the mol ratio of raw material and oxygenant is 1: 0.5～5, is 25-200 ℃ in temperature, and pressure is reaction 1-5 hour under the condition of 1-20atm.
Also can select for use as general formula (I) or metalloporphyrin (II) as Primary Catalysts, Primary Catalysts concentration is 2-500PPM, and as co-catalyst, the mol ratio of Primary Catalysts and co-catalyst is 1: 1-20 with transition metal salt or their oxide compound.
Described transition metal salt or oxide compound can be Cu, Zn, and Fe, Co, Mn, Cr, the salt of metals such as Ni or oxide compound also can be phosphoric acid salt, phosphonate, amine or ammonium salt.These co-catalysts can obviously improve the catalytic performance of metalloporphyrin Pyrogentisinic Acid preparing benzene diphenol by means of oxidation.
Substituent R on the phenyl ring
1, R
2, R
3Can be hydrogen, alkyl, alkoxyl group, hydroxyl, nitro, halogen, amido, amino, glycosyl replaces glycosyl and cyclodextrin.Dentate X can be an acetate, methyl ethyl diketone, halogen and other acid radical anions.
Atoms metal M in the general formula (I) can be Fe, Mn, and Co, Cr, Cu, Ni, Pt, Pd, Tb waits transition metal atoms; Atoms metal M in the general formula (II)
1, M
2Can be transition metal atoms such as Fe, Mn, Cr;
The carrier that constitutes supported metalloporphyrin with metalloporphyrin has: silica gel, molecular sieve, aluminum oxide, zeolite, diatomite, activated carbon, sepiolite, porous ceramics, polyvinyl chloride, polyvinyl chloride, polystyrene, Mierocrystalline cellulose, chitosan, chitin and their modifier.
When oxygenant of the present invention is NaClO, during Peracetic Acid, temperature of reaction is 25-120 ℃, and pressure is normal pressure.
When oxygenant of the present invention was air or oxygen, temperature of reaction was 100-200 ℃, and pressure is 1-20atm.
Reaction conditions gentleness of the present invention, the catalyst system therefor consumption is little, catalytic efficiency is high, and good reaction selectivity does not have corrosive nature to equipment, transformation efficiency and rate of recovery height.
Embodiment
Embodiment 1:
8mg had the metalloporphyrin of structural formula (I), R
1=R
2=R
3=CH
3, M=Mn and 20mg Cu
2Cl
2Add in the 100g phenol, add 30%H2O2 300ml.55 ℃ of following reaction stirred 3 hours, phenol conversion was 32%, pyrocatechol and Resorcinol yield 95% in the reaction product.
Embodiment 2:
5mg had the metalloporphyrin of structural formula (II), R
1=R
2=OH, R
3=Cl, M
1=M
2=Fe and 20mg sodium phosphate add in the 300ml water, add 100g 4-methylphenol and 200g NaClO.100 ℃ of following reaction stirred 4 hours, 4-methylphenol transformation efficiency was 28%, 4-methyl pyrocatechol yield 87% in the reaction product.
Embodiment 3:
5mg had the metalloporphyrin of structural formula (I), R
1=OCH
3, R
2=R
3=Br, Ml=Co and 24mg triethylamine add in the 50ml aniline, add 40% Peracetic Acid 200ml and ethanol 150ml.50 ℃ of following reaction stirred 5 hours, the aniline transformation efficiency was 30.8%, Resorcinol yield 65% in the reaction product.
Embodiment 4:
With the metalloporphyrin of the immobilized 6mg structural formula of molecular sieve (II), R
1=NO
2, R
2=R
3=H, M
1=M
2=Mn adds in the mixed system of 100ml 3-N-methyl-p-nitroaniline and 200ml acetate, slowly adds 150 gram NaClO under 110 ℃ of stirrings, reactant 2 hours, and 3-N-methyl-p-nitroaniline transformation efficiency is 28.3%, diphenol yield 90% in the reaction product.
Embodiment 5:
With the metalloporphyrin of the immobilized 4mg structural formula of polyvinyl chloride (I), R
1=R
2=N (CH
3)
2, R
3=C
2H
5, M=Cr adds in the 100g naphthalene.Add 40%H
2O
2200ml.60 ℃ of following reaction stirred 4 hours, the naphthalene transformation efficiency was 26%, naphthols yield 88% in the reaction product.
Embodiment 6:
5mg had the metalloporphyrin of structural formula (I), R
1=C
4H
9, R
2=R
3=H, M=Fe and 30mg Cobaltous diacetate add in the mixed system of 200g 1-naphthols and 300ml benzene, feeding 8atm air, and 160 ℃ of following reaction stirred 5 hours, 1-naphthols transformation efficiency was 22.5%, diphenol yield 73% in the reaction product.
Embodiment 7:
With the metalloporphyrin that 8mg has general formula (I) structure, R
1=R
2=CH
3, R
3=Cl, M=Fe, with the fine little element of 3 grams immobilized after, add in the 100ml 6-chloro-1-naphthols, feed the air of 12atm.180 ℃ of following reaction stirred 3 hours, 6-chloro-1-naphthols transformation efficiency was 30.5%, diphenol yield 85% in the reaction product.
Embodiment 8:
With the metalloporphyrin that 3mg has general formula (II) structure, R
1=R
2=H, R
3=2,3,4,6-tetrem acyl glucosyl group, M
1=M
2=Fe adds 100ml 5-methoxyl group-2-naphthylamines, 300ml ethyl acetate and 230gNaClO.80 ℃ of following reaction stirred 3 hours, 5-methoxyl group-2-naphthylamines transformation efficiency was 35%, 5-methoxynaphthol yield 86% in the reaction product.
Embodiment 9:
8mg had the metalloporphyrin of general formula (II), R
1=OC
2H
5, R
2=R
3=H, M
1=M
2=Cr and 50mgNiO add in the 100g 2-naphthylamines, feed the 15atm air.170 ℃ of following reaction stirred 5 hours, 2-naphthylamines transformation efficiency was 12.4%, naphthols yield 86% in the reaction product.
Embodiment 10:
6mg had the metalloporphyrin of general formula (I), R
1=R
2=R
3=H, M=Cu and 10mg triphenyl phosphine add 100g 3-hydroxy-acetophenone, 300ml ethyl acetate and 170g NaClO.75 ℃ of following reaction stirred 3 hours, 3-hydroxy-acetophenone transformation efficiency was 27.5%, diphenol yield 90% in the reaction product.
Claims (5)
1. the preparation method of dihydroxy-benzene and naphthols, it is characterized in that with phenol, aniline, naphthalene or their substituent are made raw material, at pH 1～13 water, acetone, ethanol, acetate, ethyl acetate, benzene is in the toluene equal solvent, select for use by the μ-oxygen bimetallic porphyrin of the monometallic porphyrin of general formula (I) or general formula (II) or above-mentioned metalloporphyrin and inorganic or immobilized thing that organic polymer constitutes separately as catalyzer, catalyst concn is 2-500PPM, uses hydrogen peroxide, clorox or air are as oxygenant, and the mol ratio of raw material and oxygenant is 1: 0.5～5, in temperature is 25-200 ℃, and pressure is reaction 1-5 hour under the condition of 1-20atm;
Substituent R on the phenyl ring
1, R
2, R
3Can be hydrogen, alkyl, alkoxyl group, hydroxyl, nitro, halogen, amido, amino, glycosyl replaces glycosyl and cyclodextrin; Dentate X can be an acetate, methyl ethyl diketone, halogen and other acid radical anions;
Atoms metal M in the general formula (I) can be Fe, Mn, and Co, Cr, Cu, Ni, Pt, Pd, Tb waits transition metal atoms; Atoms metal M in the general formula (II)
1, M
2Can be transition metal atoms such as Fe, Mn, Cr.
2. the preparation method of dihydroxy-benzene and naphthols, it is characterized in that with phenol, aniline, naphthalene or their substituent are made raw material, at pH 1 ~ 13 water, acetone, ethanol, acetate, ethyl acetate, benzene in the toluene equal solvent, is selected for use as general formula (I) or metalloporphyrin (II) as Primary Catalysts, Primary Catalysts concentration is 2-500PPM, with transition metal salt or oxide compound or phosphoric acid salt, phosphonate, amine or ammonium salt are as co-catalyst, and the mol ratio of Primary Catalysts and co-catalyst is 1: 1-20, use hydrogen peroxide, clorox or air or oxygen are as oxygenant, the mol ratio of raw material and oxygenant is 1: 0.5 ~ 5, in temperature is 25-200 ℃, and pressure is under the 1-20atm condition, condition under the reaction 1-5 hour.
3. according to the preparation method of claim 1 or 2, it is characterized in that temperature of reaction is 25-120 ℃ when using hydrogen peroxide, clorox as oxygenant, pressure is normal pressure.
4. according to the preparation method of claim 1 or 2, it is characterized in that when making oxygenant with air or oxygen that temperature of reaction is 100-200 ℃, pressure is 1-20atm.
5. according to the preparation method of claim 2, it is characterized in that described transition metal salt or oxide compound can be Cu, Zn, Fe, Co, Mn, Cr, the salt of metals such as Ni or oxide compound.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2005100320710A CN1740129A (en) | 2005-08-30 | 2005-08-30 | Prepn process of hydroquinone and phenol |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2005100320710A CN1740129A (en) | 2005-08-30 | 2005-08-30 | Prepn process of hydroquinone and phenol |
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| Publication Number | Publication Date |
|---|---|
| CN1740129A true CN1740129A (en) | 2006-03-01 |
Family
ID=36092683
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNA2005100320710A Pending CN1740129A (en) | 2005-08-30 | 2005-08-30 | Prepn process of hydroquinone and phenol |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102093169A (en) * | 2009-12-10 | 2011-06-15 | 中国科学院过程工程研究所 | Method for preparing benzenediol from hydroxylating phenol |
| CN102503752A (en) * | 2011-10-08 | 2012-06-20 | 大连理工大学 | Method for preparing polysubstituted 2-naphthol |
| CN101723808B (en) * | 2009-12-08 | 2012-07-04 | 天津大学 | Method for preparing 1-naphthol by using pigment green B catalysis |
| CN107129426A (en) * | 2016-02-29 | 2017-09-05 | 南京工业大学 | One kind 2,5- chlorophenesic acid preparation methods |
-
2005
- 2005-08-30 CN CNA2005100320710A patent/CN1740129A/en active Pending
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101723808B (en) * | 2009-12-08 | 2012-07-04 | 天津大学 | Method for preparing 1-naphthol by using pigment green B catalysis |
| CN102093169A (en) * | 2009-12-10 | 2011-06-15 | 中国科学院过程工程研究所 | Method for preparing benzenediol from hydroxylating phenol |
| CN102093169B (en) * | 2009-12-10 | 2013-06-05 | 中国科学院过程工程研究所 | Method for preparing benzenediol from hydroxylating phenol |
| CN102503752A (en) * | 2011-10-08 | 2012-06-20 | 大连理工大学 | Method for preparing polysubstituted 2-naphthol |
| CN102503752B (en) * | 2011-10-08 | 2014-04-02 | 大连理工大学 | Method for preparing polysubstituted 2-naphthol |
| CN107129426A (en) * | 2016-02-29 | 2017-09-05 | 南京工业大学 | One kind 2,5- chlorophenesic acid preparation methods |
| CN107129426B (en) * | 2016-02-29 | 2021-01-26 | 南京工业大学 | Preparation method of 2, 5-dichlorophenol |
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Open date: 20060301 |